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Liquid–Liquid Equilibrium of Sesame Fatty Acid (Ethyl and Methyl) Ester + Glycerol + Ethanol/Methanol Mixtures at Different Temperatures

dc.contributor.authorSilva, Anderson
dc.contributor.authorLopes, Guilherme [UNESP]
dc.contributor.authorCorazza, Marcos
dc.contributor.authorArce, Pedro
dc.contributor.authorCoêlho, Dayana
dc.contributor.authorMeili, Lucas
dc.contributor.authorCarvalho, Sandra
dc.contributor.authorFerreira-Pinto, Leandro
dc.contributor.authorSoletti, João
dc.contributor.institutionFederal University of Alagoas
dc.contributor.institutionUniversidade Estadual Paulista (UNESP)
dc.contributor.institutionFederal University of Parana
dc.contributor.institutionUniversidade de São Paulo (USP)
dc.date.accessioned2025-04-29T20:10:55Z
dc.date.issued2024-07-01
dc.description.abstractThis study aimed to investigate the liquid–liquid equilibrium (LLE) behavior of sesame fatty acid ethyl ester (FAEE) and methyl ester (FAME) in combination with glycerol and the co-solvents ethanol and methanol. FAEE and FAME were produced through the transesterification of mechanically extracted and purified sesame oil, using potassium hydroxide (KOH) as a homogeneous base catalyst. The reactions were conducted in ethanol and methanol to produce FAEE and FAME, respectively. Post-reaction, the products were separated and purified, followed by an analysis of the LLE behavior at 313.15 K and 323.15 K under atmospheric pressure (101.3 kPa). The experimental process for the miscibility analysis utilized a jacketed glass cell adapted for this study. Miscibility limits or binodal curves were determined using the turbidity-point method. Tie lines were constructed by preparing mixtures of known concentrations within the two-phase region, which allowed the phases to separate after agitation. Samples from both phases were analyzed to determine their composition. This study revealed that higher temperatures promoted greater phase separation and enhanced the biodiesel purification process. The NRTL model effectively correlated the activity coefficients with the experimental data, showing good agreement, with a root-mean-square deviation of 3.5%. Additionally, the data quality was validated using Marcilla’s method, which yielded an R2 value close to 1. Attraction factors and distribution coefficients were also calculated to evaluate the efficiency of the co-solvents as extraction agents. The findings indicated higher selectivity for methanol than for ethanol, with varying degrees of distribution among the co-solvents. These results offer significant insights into enhancing biodiesel production processes by considering the effects of co-solvents on the LLE properties of mixtures, ultimately contributing to more efficient and cost-effective biodiesel production.en
dc.description.affiliationLaboratory of Separation Systems and Process Optimization (LASSOP) Center of Technology Federal University of Alagoas, AL
dc.description.affiliationDepartment of Engineering School of Engineering and Sciences Sao Paulo State University (UNESP), SP
dc.description.affiliationDepartment of Chemical Engineering Federal University of Parana, PR
dc.description.affiliationDepartment of Chemical Engineering Engineering School of Lorena (EEL/USP) University of Sao Paulo, SP
dc.description.affiliationUnespDepartment of Engineering School of Engineering and Sciences Sao Paulo State University (UNESP), SP
dc.identifierhttp://dx.doi.org/10.3390/molecules29133167
dc.identifier.citationMolecules, v. 29, n. 13, 2024.
dc.identifier.dimensionspub.1173532875
dc.identifier.doi10.3390/molecules29133167
dc.identifier.issn1420-3049
dc.identifier.issn1431-5157
dc.identifier.lattes3625079127976189
dc.identifier.orcid0000-0002-4687-5297
dc.identifier.orcid0000-0003-2305-1989
dc.identifier.orcid0000-0002-0307-8204
dc.identifier.orcid0000-0003-2891-3859
dc.identifier.orcid0009-0000-2068-2043
dc.identifier.orcid0000-0002-0656-9471
dc.identifier.pmcidPMC11243479
dc.identifier.pmid38999119
dc.identifier.scopus2-s2.0-85198469229
dc.identifier.urihttps://hdl.handle.net/11449/307981
dc.language.isoeng
dc.publisherMDPI
dc.relation.ispartofMolecules
dc.rights.accessRightsAcesso abertopt
dc.rights.sourceRightsoa_all
dc.rights.sourceRightsgold
dc.sourceScopus
dc.sourceDimensions
dc.subjectalcohol
dc.subjectbiodiesel
dc.subjectliquid–liquid equilibrium
dc.subjectNRTL
dc.subjectsesame oil
dc.titleLiquid–Liquid Equilibrium of Sesame Fatty Acid (Ethyl and Methyl) Ester + Glycerol + Ethanol/Methanol Mixtures at Different Temperaturesen
dc.typeArtigopt
dspace.entity.typePublication
relation.isAuthorOfPublication6fceb91d-f272-400a-8040-74a7906258f6
relation.isAuthorOfPublication.latestForDiscovery6fceb91d-f272-400a-8040-74a7906258f6
unesp.author.orcid0009-0000-2068-2043[1]
unesp.author.orcid0000-0001-7331-8173[2]
unesp.author.orcid0000-0003-2305-1989[3]
unesp.author.orcid0000-0002-4687-5297[4]
unesp.author.orcid0000-0002-5170-3449[5]
unesp.author.orcid0000-0002-0307-8204[6]
unesp.author.orcid0000-0003-2891-3859[7]
unesp.author.orcid0000-0002-7758-9939[9]

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